JP4328880B2 - Garbage disposal method and equipment - Google Patents

Garbage disposal method and equipment Download PDF

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JP4328880B2
JP4328880B2 JP14269399A JP14269399A JP4328880B2 JP 4328880 B2 JP4328880 B2 JP 4328880B2 JP 14269399 A JP14269399 A JP 14269399A JP 14269399 A JP14269399 A JP 14269399A JP 4328880 B2 JP4328880 B2 JP 4328880B2
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garbage
sludge
tank
biological treatment
raw
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JP2000325993A (en
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清一 二星
公昭 服部
茂 黒木
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清一 二星
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/20Sludge processing

Description

【0001】
【発明の属する技術分野】
この発明は、一般家庭で生じる生ゴミをはじめ食品工場やホテルやレストランなどで生じる生ゴミを処理して、最終的に下水道や河川などに排水として放流したり、中水道としての利用も可能な生ゴミ処理の方法と同設備(システム)に関するものである。なお、生ゴミは野菜屑や果物のかす、魚の頭や骨など、主として台所や厨房で生じる食べ物の残りかすをいう。
【0002】
【従来の技術】
生ゴミの処理として一般的に行われている方法は、▲1▼焼却処分、▲2▼コンポスト化、▲3▼炭化農地還元、▲4▼微生物による消滅処理の四つに分類される。
【0003】
【発明が解決しようとする課題】
しかしながら、上記した▲1▼〜▲4▼の生ゴミ処理方法には、次のような種々の問題がある。
【0004】
▲1▼ 焼却処分:
200℃以上の高温での焼却によりダイオキシンなどの二次公害が発生するおそれがあり、これを避けるために高湿状態で低温焼却するには、膨大なエネルギーが必要で、処理コストが非常に高くなる。また、焼却した灰を埋め立てるための処分場として広大な用地を確保しなければならないうえに、焼却時に悪臭が発生することがあって、周辺の環境に悪影響を及ぼすおそれがある。
【0005】
▲2▼ コンポスト化:
地方都市では十分に土地があるために、コンポスト化は可能であるが、大都市やその周辺では、コンポスト化するための用地の確保が困難なうえに、周辺の住民の同意を得る必要があり、また生ゴミの運搬や商品化に対する流通過程上での問題がある。これらに加えて、微生物による処理過程で悪臭が発生するという問題もある。
【0006】
▲3▼ 炭化農地還元:
近年、生ゴミを炭化処理する方法が開発されているが、生ゴミは無機物に限られず、有機物も含まれるために、炭化過程で有毒ガスが発生したり、悪臭が発生したりする可能性がある。また、炭化して農地還元する場合にも、流通上の問題があるほか、毎日発生する生ゴミを消費者側がどの程度受け入れることができるかの問題が残る。
【0007】
▲4▼ 微生物による消滅処理
この処理方法は前処理として無機物を除去してから投入する必要があり、また生ゴミの投入量に対し微生物菌群を9倍(重量)の割合で多量に必要とする装置からなるために、装置自体が広い設置場所を占有する。しかも、生ゴミの種類によっては、1週間〜1カ月経過しても、生ゴミの分解が進行しないことがある。
【0008】
また、生ゴミの塩分濃度が高くなるにつれて、定期的(普通は1年に3〜4回)に微生物菌群(オガクズを含む)を入れ替えなければならないうえに、微生物菌群は産業廃棄物として処分されることになるので、処分上の問題がある。さらに、生ゴミを所定割合以上に投入し過ぎると、腐敗・悪臭が発生するという問題がある。
【0009】
この発明は上述の点に鑑みなされたもので、生ゴミを雑排水と同じように水処理に近似の方法で処理することにより、ダイオキシン等の二次公害の発生を防止し、処理設備周辺での悪臭等の発生がなく、環境を悪化させることがなく、設備コストも比較的安価な生ゴミ処理方法と同処理設備を提供することを目的としている。また、生ゴミに混合する水は処理後に中水道としての利用が可能で、しかも処理過程で発生する汚泥も、土壌改良剤として利用できるようにして廃棄物を無くすか最小限に抑えることも目的としている。
【0010】
【課題を解決するための手段】
上記の目的を達成するためにこの発明に係る生ゴミ処理方法は、生ゴミに腐植土を含む汚泥を混合して貯留し、この貯留した生ゴミの数倍の重量の水を生ゴミに加えて粉砕し、液状化した生ゴミ汚水を空気を導入しながら一定期間貯留したのち、
腐植土を含む前記汚泥を混合撹拌して所定濃度に保った生物処理槽へ前記生ゴミ汚水を所定流量ずつ供給し、該生物処理槽内で前記生ゴミ汚水を、空気を導入して通気しながら前記汚泥中の微生物により分解処理したのち、固液分離して得られる処理水を下水道もしくは河川などに放流することを特徴としている。
【0011】
上記の構成を有する本発明に係る生ゴミ処理方法によれば、生ゴミを貯留する際に腐植土を含む汚泥を混合することにより、汚泥又は腐植土中に含まれている土壌菌群(通性嫌気バクテリアと、好気性バクテリア若しくは通性嫌気バクテリアおよび好気性バクテリアなど)により脱臭作用が発揮されることから、生ゴミの貯留時に悪臭がほとんど発生しない。そして、貯留された生ゴミが一定量(満杯)に達すると、数倍の水を生ゴミに加えて粉砕し、液状化した状態で粉砕された生ゴミ汚水に汚泥がさらに混合され、これに空気が導入されて通気されることにより、汚泥中の微生物によって生ゴミがある程度分解されると同時に、上記したとおり混合された汚泥により悪臭の発生も抑制される。また、生ゴミの数倍の水が加えられ、しかも生ゴミは細かく粉砕され液状化されているから、排水(生ゴミ汚水)に近い状態でポンプ等により生物処理槽へ簡単にかつスムーズに供給(給水)できるとともに、供給する生ゴミ汚水の流量を流量計等により正確に測定しながら、所定流量ずつ生物処理槽へ簡単に供給できるので、汚泥の濃度を生ゴミの生物処理に最適な状態に維持できる。また生物処理槽では、空気が導入されて通気されることにより、汚泥中の微生物の活動(分解作用)が促進されることによって生ゴミが効率的に短期間で分解される。
【0012】
そして、生物処理槽内で主に水分と二酸化炭素とに分解され、固液分離して得られる処理水は下水道や河川に放流するか、さらに消毒処理を施すことによって中水道として再使用可能になる。また、固液分離して得られる固形物としての汚泥は、生ゴミの大部分が二酸化炭素と水分に分解されることにより、発生しても少量で、これらが余剰汚泥になる。そして、生物処理槽内の汚泥の一部を、貯留する生ゴミに最初に混合して脱臭と分解処理に供するために循環して使用されるとともに、循環途中で腐植土が投入されて活性化される。
【0013】
上記の目的を達成するためにこの発明に係る生ゴミ処理設備(請求項3)は、生ゴミを投入するとともに腐植土を含む汚泥とともに生ゴミの数倍の重量の水を加えて貯留する生ゴミ受入れホッパーと、該ホッパー内の生ゴミを搬送するコンベヤ装置と、該コンベヤ装置の先端に連設され、粉砕して液状化する生ゴミ粉砕機と、粉砕、液状化された生ゴミ汚水を貯留する貯留槽と、該貯留槽内の生ゴミ汚水を所定量ずつ計量しながら生物処理槽へ供給する計量器と、腐植土を含む前記汚泥を前記生ゴミ汚水に混合、撹拌させた前記生物処理槽と、腐植土供給機を備え前記生物処理槽内の汚泥の一部を送給(送り戻)して貯留しながら活性化させる汚泥培養槽と、前記ホッパー内から臭気をあるいは大気中から空気を吸引し、前記貯留槽、前記生物処理槽および前記汚泥培養槽に空気を送給する曝気用ブロワーと、前記生物処理槽内に配備される固液分離機構とを具備したことを特徴としている。
【0014】
上記の構成を有する本発明の生ゴミ処理設備は、上記の処理方法を確実に実施できるほか、構成部材が比較的少なく構造が簡単である。また、前記生物処理槽内の汚泥の一部は、汚泥培養槽へ送られ、そこで腐植土供給機により導入される腐植土中の土壌菌の繁殖により汚泥が熟成し活性化される。なお、活性化された汚泥は、貯留タンクへ送られ、生物処理槽および生ゴミ受入れホッパーも送られて、最終的には循環される。
【0015】
上記の請求項1に記載の生ゴミ処理方法において請求項2に記載のように、前記生物処理槽の汚泥濃度を、 5000〜15000mg/lに設定することが望ましい。また、上記の請求項3に記載の生ゴミ処理設備において請求項4に記載のように、前記生物処理槽の汚泥濃度を、 5000〜15000mg/lに設定することが望ましい。
【0016】
請求項2に記載の生ゴミ処理方法又は請求項4に記載の生ゴミ処理設備によれば、汚泥濃度を 5000〜15000mg/lに設定したことにより、生ゴミの生物処理に必要かつ十分な汚泥濃度が確保されるとともに、余剰汚泥の発生が最小限に抑えられる。
【0017】
ところで、本明細書で腐植土とは、土壌や石炭などに含まれる動植物が分解してできた黒褐色の有機質からなる腐植を多量に含む土質をいい、詳しくは、腐植(土)は植物や動物が微生物によって分解され、炭酸ガス、水、アンモニア等の無機ガスとともに、糖類、キノン類、アミノ酸、タンパク質等の低分子有機物ができ、これらの低分子有機物が脱水結合を繰り返して高分子の再合成産物となるが、この再合成産物と分解途上および未分解有機物の総称である。
【0018】
また、腐植土の種類については特に限定するものではないが、落葉樹の落ち葉と動物由来の分解物が温暖な気候の下で十分に分解され、それから再合成物となったのちに、カルシウムで飽和されてできた中性腐植を原料とし、バイオテクノロジーによって低分子化し、量を増やしてミセルコロイドとして安定化させた腐植土を使用するのが望ましい。中性腐植は8000年間地中に密閉埋蔵されてできた腐植であり、微生物によって分解される栄養型腐植の量が多く、バイオテクノロジーによって産生されるフルボ酸および鉄錯体の含有量が数10%に及ぶから好適である。
【0019】
【発明の実施の形態】
以下、この発明に係る生ゴミ処理設備の実施の形態を図面に基づいて説明し、併せて同処理設備による生ゴミの処理方法についても説明する。
【0020】
図1はこの発明の生ゴミ処理設備の実施例を示す設備全体のフローチャート図である。
腐植土Jを含む活性化した汚泥Hを媒介として生ゴミBを生物処理する生ゴミ処理設備1は、図1に示すように、生ゴミ受入れホッパー2、生ゴミ汚水貯留タンク(貯留槽)3、生物処理槽4、汚泥培養槽5、腐植土供給機6および消毒槽7を備えている。
【0021】
生ゴミ受入れホッパー2は、上端開口を上壁面2aにより閉塞し、上壁面2aの一部に生ゴミBの投入口2bを備え、この投入口2bには蓋21が開閉可能に取り付けられている。上壁面2aの中央部には、臭気の吸引口26が穿設され、吸引口26には臭気吸引管27の一端が接続されている。またホッパー2の下端2cは開口されており、この下端開口2cにスクリューコンベヤ23の後部側がコンベヤ23内部に連通して配備されている。スクリューコンベヤ23は、生ゴミ汚水貯留タンク3の上方まで延設され、スクリューコンベヤ23の前端には生ゴミ粉砕機31が連設されている。またスクリューコンベヤ23の後端には、スクリュー24の駆動用モータ25が装着されている。粉砕機31は上端に駆動用モータ32を備え、下端開口から導入筒33を下方へ延設している。さらに、生ゴミBを排水と同じように水処理するため、清水(上水道の水を含む)を生ゴミ受入れホッパー2内に給水するための給水管11の一端が、上壁面2aを貫通して挿入されている。給水管11の他端は給水源(図示せず)に接続されている。
【0022】
貯留タンク3は、上端開口を上壁面3aにより閉塞した密閉式タンクで、粉砕機31の導入筒33が上壁面3aを貫通して内部に臨ませてある。また上壁面3aの中央部には、臭気の吸引口34が穿設され、吸引口34には臭気吸引管35の一端が接続されている。貯留タンク3の側壁3bの下端部付近に生ゴミ汚水Cの排出管36が接続され、この排出管36には供給ポンプ40が介設され、生ゴミ汚水Cの供給流量を計測する計量器(流量計)8の入口に排出管36の下流端が接続されている。また計量器8には、あらかじめ設定した流量(単位時間当たり)をオーバーフローした生ゴミ汚水Cを貯留タンク3へ戻すための排水管37の一端が接続され、排水管37の他端は貯留タンク3の側壁3bの上端部に接続されている。さらに計量器8の流出口から生ゴミ汚水Cの供給管38が、生物処理槽4内に臨ませてある。臭気吸引管35の他端は臭気吸引管27の途中に接続され、臭気吸引管27の他端がブロワ30の吸引口に接続されている。
【0023】
生物処理槽4は上端が開口されており、貯留された生ゴミ汚水Cの水量に対して、本例では5000〜15000mg/lの汚泥濃度の範囲になるように、腐植土Jを含む汚泥Hがあらかじめ投入されている。また、生物処理槽4内の底部付近には水中ポンプ41が配備され、底部に沈殿している汚泥Hを生ゴミ受入れホッパー2内へ供給できるように、水中ポンプ41の吐出口に汚泥供給管42の一端が接続され、汚泥供給管42の他端が生ゴミ受入れホッパー2の上壁面2aに接続されている。生物処理槽4の側壁4aの上端部には汚泥Hの排出管43の一端が接続され、他端が汚泥培養槽5の側壁5bの上端部に接続されている。さらに、生物処理槽4内には生ゴミ汚水C中から固形分としての汚泥Hを分離し、浄化された処理水xを取り出すための液中膜装置9が配備されている。この液中膜装置9の底部には、ブロワ30の吐出口に一端が接続された空気導入管91の他端が接続され、液中膜装置9を空気導入管91から吐出される空気(臭気を含む)で振動させ、固液分離を促進すると同時に、生ゴミ汚水C中に空気の気泡を吐出させ、汚泥H中の微生物に通気して空気のと接触させる。なお、生物処理槽4は上端を開口してあるので、生ゴミ汚水Cの上面は空気と接触している。
【0024】
液中膜装置9の上端には、処理水xの吸引供給管71の一端が接触され、吸引供給管71の途中に供給ポンプ72が介設され、吸引供給管71の他端は消毒槽7の処理水x中に臨ませてある。消毒槽7内において、吸引供給管71の出口のすぐ下方に、固形消毒剤(本例では、次亜塩素酸ソーダ)sの収納容器73が設置され、収納容器73に設けられた多数の小孔から固形消毒剤sが処理水xに溶解する。消毒剤sの溶解濃度は、本例では10PPM 前後に設定されている。こうして、消毒された処理水yは、本例では下水道や河川等に放流されるが、中水道として再利用することも可能である。
【0025】
一方、生物処理槽4内の汚泥Hを生ゴミ受入れホッパー2へ汚泥供給管42により供給するのとは別に、排出管43からも汚泥Hが汚泥培養槽5へ送給される。汚泥培養槽5は上端開口が上壁面5aで閉塞され、腐植土供給機6から汚泥培養槽5内の汚泥Hに腐植土Jが定期的に供給される。腐植土供給機6は、腐植土Jを上端の投入口62から収納したホッパー状容器61と、容器61の下端開口63に連通して配設されたスクリューコンベヤ64と、スクリューコンベヤ64の前端から下向けに延設され、上壁面5aを貫通して汚泥培養槽5内の汚泥Hに臨ませた導入筒67とを備えている。また腐植土供給機6は、後端に装備したモータ66で回転するスクリュー65を具備している。なお汚泥培養槽5内の汚泥濃度は、本例では5000〜15000mg/l前後に設定されている。また生物処理槽4から汚泥培養槽5へ送給される汚泥Hの量は、1日間(24時間)に生ゴミ受入れホッパー2へ投入される生ゴミBの重量の50〜100重量%である。さらに汚泥培養槽5内の汚泥Hの活性化のために腐植土供給機6から供給される腐植土Jの供給は、20日〜30日間に1回の割合で行われ、1回の供給量は生ゴミBの投入量の0.5〜2.0重量%である。このため、腐植土供給機6にはタイマー(図示せず)が装備され、定期的に一定時間だけモータ66によりスクリュー65が回転する。
【0026】
汚泥培養槽5の側壁5bの上下方向の中間位置から、活性化された汚泥Hを貯留タンク3へ供給するため、汚泥供給管51が貯留タンク3の側壁3bの上端部に接続されている。また、汚泥排出管43の途中で分岐された分岐管44の一端も貯留タンク3の側壁の上端部に接続され、生物処理槽4内の余剰汚泥Hも分岐管44を通って貯留タンク3へ供給される。
【0027】
そのほか、ブロワ30の吐出口から延びる空気導入管91は途中で分岐され、分岐管92が消毒槽7の処理水xの底部付近まで挿入され、分岐管92の下端に接続された空気吹出しノズル93から気泡状の空気が処理水x中に導入される。また、空気導入管91は分岐管92のすぐ下流側で分岐され、この分岐管94が貯留タンク3の上壁面3aを貫通して生ゴミ汚水Cの底部付近まで挿入され、分岐管94の下端に接続された空気吹出しノズル95から気泡状の空気が生ゴミ汚水C中に導入される。さらに、分岐管94は途中で分岐され、この第2分岐管96が汚泥培養槽5の上壁面5aを貫通し、汚泥H中の底部付近まで挿入され、第2分岐管96の下端に接続された空気吹出しノズル97から気泡状の空気が汚泥H内に導入される。
【0028】
次に、上記構成の生ゴミ処理設備の実施例についてその作動状況(生ゴミ処理方法)を説明する。
【0029】
1) 例えば、マンション、アパート等の集合住宅あるいは食品工場、ホテル、レストランなどから発生する多量の生ゴミBが、直接にあるいは生ゴミ収集トラック等で搬送されて生ゴミ受入れホッパー2へ投入される。
【0030】
2) 生ゴミ受入れホッパー2へは、給水管11から清水が生ゴミBの投入量の2〜3倍(重量)が供給される。また生物処理槽4内の汚泥Hが水中ポンプ41を介して、汚泥供給管42により生ゴミ受入れホッパー2へ供給される。汚泥Hの供給量は、生ゴミBと水の重量の30%前後であり、汚泥Hが生ゴミCに混合されることにより、汚泥中の土壌菌群が代謝産物を産出するが、その代謝産物は、好気性細菌、通性嫌気性細菌、若しくは好気性細菌と通性嫌気性細菌からなる細菌群の分泌物で、臭気除去成分を有し、生ゴミCから発生する臭気ガスは汚泥Hと接触し、ガス中の臭成分と反応し分解して、臭成分の発散を防止して脱臭させる。また、空気が導入されて通気されることにより、汚泥Hに含有されている好気性バクテリア、通性嫌気性バクテリア、若しくは好気性バクテリアと通性嫌気性バクテリアからなるバクテリア群により、生ゴミBの一部が分解される。
【0031】
3) 生ゴミ受入れホッパー2内の生ゴミBが水および汚泥Hと混合され、下端のスクリューコンベヤ23によって混合・撹拌されながら先端の粉砕機31へ搬送される。そして、粉砕機31によって生ゴミBは細かく粉砕され、汚泥Hと混合された状態で清水も加えられて液状化され、生ゴミ汚水Cとなって貯留タンク3内に貯留される。貯留タンク3内では、生ゴミ汚水Cに対しその30重量%の汚泥Hが、生物処理槽4および汚泥培養槽6から供給され、空気が導入されて通気されることにより、汚泥Hに含有されている好気性バクテリア、通性嫌気性バクテリア、若しくは好気性バクテリアと通性嫌気性バクテリアからなるバクテリア群により生ゴミ汚水Cの分解と悪臭の発生が防止される。特に汚泥培養槽6から供給される汚泥Hは腐植土Jの投入により活性化されているため、消臭(脱臭)効果および分解作用が優れている。
【0032】
4) 生ゴミBの粉砕物がある程度分解され、汚水(排水)に近い状態となり、この生ゴミ汚水Cが計量器で所定流量ずつ計量されながら供給ポンプにより生物処理槽4へ供給される。生物処理槽4では、空気が導入されて通気されることにより、汚泥H中の微生物(土壌菌など)によって生ゴミBの粉砕物が分解される。そして、生物処理槽4内でほぼ完全に分解され、二酸化炭素と水(処理水)になる。生物処理槽4内の処理水xと汚泥Hは、ブロワ30から送給される空気により振動する液中膜装置9によって処理水xが汚泥Hから分離されて供給ポンプ72により吸引され、消毒槽7へ送られる。なお、液中膜装置9によって分離された処理水xが、下水道への放流基準値以下(例えばBOD:200mg/l,SS:200mg/lおよびn−ヘキサン:10mg/l以下)であれば、消毒槽7へ送水せずに処理水xを下水道や河川に直接に放流することができる。
【0033】
5) 消毒槽7内において、処理水xは10PPM 前後の濃度に次亜塩素酸ソーダsが溶解された液中で、空気吹出しノズル93から気泡状の空気が通気されることによって、さらに消毒処理された処理水yが排水管75から排水され、放流される。
【0034】
なお、生物処理槽4から汚泥培養槽5へ送られた汚泥Hは、腐植土供給機6から供給された腐植土Jと混合され、汚泥培養槽5内において汚泥Hは腐植土J中に含まれている土壌菌の働きによって熟成し腐植活性化する。また、本例において汚泥Hに腐植土供給機6から供給して活性化するために用いた腐植土Jは、有機質含有量が20重量%以上で腐植酸を含み、水溶液でPH3以下、酸化還元電位が+500mmV以上であったが、これに限定するものではないことは言うまでもない。
【0035】
別の実施例
上記に本発明の生ゴミ処理設備に関する一実施例について説明したが、下記のように実施することができる。すなわち、
▲1▼ マンション等の集合住宅の各戸の台所に、粉砕機(ディスポーザ)を備え付けておき、生ゴミBを粉砕機で粉砕しながら上水道の水を加えて排水管を利用して生ゴミ汚水貯留タンク3へ直接に、生ゴミBを粉砕し水を加えて液状化した、生ゴミ汚水Cとして送る。そして、生ゴミ汚水貯留タンク3に汚泥Hとくに活性化した汚泥Hを供給し、生ゴミ汚水Cに混合して微生物による生ゴミBの分解および脱臭を行う。この場合には、生ゴミ受入れホッパー2および生ゴミ粉砕機31付きクリューコンベヤ23が不要になる。
【0036】
▲2▼ 生物処理槽4では余剰汚泥の発生を極力抑えているが、通常は余剰の汚泥が発生するので、この汚泥Hは循環させる分を除き脱水処理して貯蔵するか、汚泥培養槽5で腐植土Jを混合撹拌して活性化させたのちに、脱水・乾燥させて土壌改良剤として利用することもできる。
【0037】
【発明の効果】
以上説明したことから明らかなように、この発明に係る生ゴミ処理方法および処理設備は、下記の効果を有する。
【0038】
(1) 請求項1記載の発明は生ゴミを雑排水と同じように水処理として処理できるので、処理設備が比較的簡単で、また汚泥中の微生物により生ゴミを生物分解するので、ダイオキシン等の二次公害の発生が防止されるとともに、処理設備周辺での悪臭等の発生がなく、環境を悪化させることがない。さらに、生ゴミの混合する水は処理後に中水道としての利用が可能で、しかも処理過程で発生する汚泥も、土壌改良剤として利用できるので、廃棄用地や埋設用地が不要で、都市部での実施が可能である。
【0039】
その他、主に汚泥を脱臭および生物分解媒介として使用するので、維持管理費が安くつき、また汚泥を汚泥培養槽で活性化させながら循環させるので、脱臭および生物分解作用が低下せず半永久的に使用できる。
【0040】
(2) 請求項2記載の発明は、請求項1の処理方法を確実に実施でき、請求項1に関する上記の効果とほぼ同様の効果を奏するほか、構成部材が比較的少なく構造が簡単で、設備コストも比較的安価である。
【0041】
(3) 請求項3記載の発明では、汚泥濃度を 5000〜15000mg/lに設定したことにより、生ゴミの生物処理に必要かつ十分な汚泥濃度が確保されるとともに、余剰汚泥の発生が最小限に抑えられる。
【図面の簡単な説明】
【図1】本発明の生ゴミ処理設備の実施例を示す設備全体のフローチャート図である。
【符号の説明】
1 生ゴミ処理設備
2 生ゴミ受入れホッパー
3 生ゴミ汚水貯留タンク
4 生物処理槽
5 汚泥培養槽
6 腐植土供給機
7 消毒槽
8 計量器(流量計)
9 液中膜装置
23・64 スクリューコンベヤ
27・35 臭気供給管
30 ブロワ
31 生ゴミ粉砕機
36・43 排出管
37 排水管
40・72 供給ポンプ
42 汚泥供給管
43 汚泥供給管
44・92・94・96 分岐管
51 汚泥供給管
61 ホッパー状容器
71 吸引供給管
91 空気導入管
93・95・97 空気吹出しノズル
H 汚泥
J 腐植土
B 生ゴミ
C 生ゴミ汚水
x 処理水
y 処理水
s 消毒剤(次亜塩素酸ソーダ)
[0001]
BACKGROUND OF THE INVENTION
This invention treats raw garbage generated in general households as well as food factory, hotel, restaurant, etc., and can finally be discharged as drainage into sewers and rivers, or can be used as middle water The present invention relates to a garbage disposal method and the same equipment (system). In addition, raw garbage refers to the residue of foods produced mainly in the kitchen and kitchen, such as vegetable waste, fruit residue, fish heads and bones.
[0002]
[Prior art]
The methods generally used for the treatment of raw garbage are classified into four categories: (1) incineration, (2) composting, (3) carbonized farmland reduction, and (4) annihilation by microorganisms.
[0003]
[Problems to be solved by the invention]
However, the above garbage disposal methods (1) to (4) have the following various problems.
[0004]
(1) Incineration disposal:
Secondary pollution such as dioxins may occur due to incineration at a high temperature of 200 ° C or higher, and in order to avoid this, enormous energy is required to incinerate at high humidity and low temperature, and the processing cost is very high. Become. In addition, a vast site must be secured as a disposal site for landfilling incinerated ash, and a bad odor may be generated during incineration, which may adversely affect the surrounding environment.
[0005]
(2) Composting:
Since there is enough land in local cities, composting is possible, but in large cities and their surroundings, it is difficult to secure land for composting and it is necessary to obtain the consent of the surrounding residents Also, there are problems in the distribution process for the transportation and commercialization of garbage. In addition to these, there is also a problem that malodor is generated in the process of treatment with microorganisms.
[0006]
(3) Carbonized farmland return:
In recent years, methods for carbonizing raw garbage have been developed. However, since raw garbage is not limited to inorganic substances, but also contains organic substances, there is a possibility that toxic gases may be generated or bad odors may be generated during the carbonization process. is there. In addition, when carbonized and returned to farmland, there are problems in terms of distribution, as well as how much consumers can accept daily garbage generated.
[0007]
(4) Microbial extinction treatment This treatment method needs to be introduced after removing inorganic substances as a pretreatment, and a large amount of microorganisms are required at a rate of 9 times (weight) with respect to the input amount of garbage. The device itself occupies a wide installation place. Moreover, depending on the type of garbage, the decomposition of garbage may not proceed even after one week to one month.
[0008]
Moreover, as the salinity of raw garbage increases, the microbial group (including sawdust) must be replaced regularly (usually 3-4 times a year), and the microbial group is treated as industrial waste. Since it will be disposed, there is a problem in disposal. Furthermore, there is a problem that spoilage and bad smell occur when raw garbage is thrown in at a predetermined rate or more.
[0009]
This invention has been made in view of the above points, and by treating raw garbage in a manner similar to water treatment in the same way as miscellaneous wastewater, it prevents secondary pollution such as dioxins and the like around the treatment facility. It is an object of the present invention to provide a raw garbage processing method and the same processing equipment that do not cause odors and the like, do not deteriorate the environment, and have a relatively low equipment cost. In addition, water mixed with raw garbage can be used as a sewer after treatment, and sludge generated in the treatment process can also be used as a soil conditioner to eliminate or minimize waste. It is said.
[0010]
[Means for Solving the Problems]
In order to achieve the above object, a garbage disposal method according to the present invention stores and mixes garbage containing sludge containing humus soil and adds water several times the weight of the stored garbage to the garbage. After smashing and liquefying raw garbage wastewater for a certain period while introducing air,
The raw garbage sewage is supplied at a predetermined flow rate to a biological treatment tank in which the sludge containing humus soil is mixed and stirred and maintained at a predetermined concentration, and the raw garbage sewage is introduced into the biological treatment tank by introducing air. However, it is characterized in that after being decomposed by microorganisms in the sludge, treated water obtained by solid-liquid separation is discharged into a sewer or a river.
[0011]
According to the garbage processing method according to the present invention having the above-described configuration, the soil fungi (consumable) contained in the sludge or the humus soil are mixed by mixing the sludge containing the humus soil when the garbage is stored. Deodorizing action is exerted by sexual anaerobic bacteria and aerobic bacteria or facultative anaerobic bacteria and aerobic bacteria), so that almost no bad odor is generated when storing garbage. When the stored garbage reaches a certain amount (full), several times more water is added to the garbage and pulverized, and sludge is further mixed with the crushed garbage wastewater in a liquefied state. When air is introduced and ventilated, garbage is decomposed to some extent by microorganisms in the sludge, and at the same time, generation of malodor is suppressed by the mixed sludge as described above. In addition, water several times the amount of raw garbage is added, and the raw garbage is finely pulverized and liquefied, so it can be easily and smoothly supplied to the biological treatment tank by a pump etc. in a state close to wastewater (garbage wastewater). (Water supply) In addition to accurately measuring the flow rate of raw garbage sewage with a flow meter etc., it can be easily supplied to the biological treatment tank at a predetermined flow rate, so the sludge concentration is optimal for biological treatment of raw garbage. Can be maintained. In the biological treatment tank, air is introduced and ventilated to promote the activity (decomposition action) of microorganisms in the sludge, so that the garbage is efficiently decomposed in a short period of time.
[0012]
And it is decomposed mainly into water and carbon dioxide in the biological treatment tank, and the treated water obtained by solid-liquid separation can be reused as sewerage by discharging it into sewers and rivers or by disinfecting it further. Become. Further, sludge as solid matter obtained by solid-liquid separation is a small amount even if it is generated when most of raw garbage is decomposed into carbon dioxide and moisture, and these become excess sludge. A part of the sludge in the biological treatment tank is first mixed with the stored garbage and used for deodorization and decomposition treatment. At the same time, humus soil is introduced and activated. Is done.
[0013]
In order to achieve the above object, the garbage processing facility according to the present invention ( Claim 3 ) is provided with raw garbage that is charged and stored with sludge containing humus soil and water several times the weight of garbage. A garbage receiving hopper, a conveyor device for conveying garbage in the hopper, a garbage crusher connected to the tip of the conveyor device for pulverization and liquefaction, and crushed and liquefied garbage waste water A storage tank to be stored, a measuring instrument for feeding the garbage wastewater in the storage tank to the biological treatment tank while measuring a predetermined amount, and the living organism in which the sludge containing humus soil is mixed and stirred in the garbage wastewater. A treatment tank, a sludge culture tank that is provided with a humus soil supply machine and activated while storing (feeding back) a part of the sludge in the biological treatment tank, and odor from the hopper or from the atmosphere Air is sucked into the storage tank, the raw It comprises an aeration blower for supplying air to a material treatment tank and the sludge culture tank, and a solid-liquid separation mechanism provided in the biological treatment tank.
[0014]
The garbage processing facility of the present invention having the above-described configuration can implement the above-described processing method reliably, and has a relatively small number of constituent members and a simple structure. A part of the sludge in the biological treatment tank is sent to a sludge culture tank, where the sludge is matured and activated by the propagation of soil bacteria in the humus soil introduced by the humus soil supply machine. The activated sludge is sent to the storage tank, the biological treatment tank and the garbage receiving hopper are also sent, and finally circulated.
[0015]
In the garbage disposal method according to claim 1, as described in claim 2, it is desirable to set a sludge concentration in the biological treatment tank to 5000 to 15000 mg / l. Moreover, in the garbage processing facility according to claim 3, the sludge concentration in the biological treatment tank is preferably set to 5000 to 15000 mg / l as described in claim 4.
[0016]
According to the garbage disposal method according to claim 2 or the garbage disposal facility according to claim 4, by setting the sludge concentration to 5000-15000 mg / l, the sludge necessary and sufficient for biological treatment of garbage Concentration is ensured and the generation of excess sludge is minimized.
[0017]
By the way, humus soil in this specification means soil quality that contains a large amount of black-brown organic humus made by decomposing animals and plants contained in soil and coal. Specifically, humus (soil) is a plant or animal. Is decomposed by microorganisms, and together with inorganic gases such as carbon dioxide, water, and ammonia, low molecular organic substances such as sugars, quinones, amino acids, and proteins are formed, and these low molecular organic substances repeat dehydration to re-synthesize polymers. Although it is a product, it is a collective term for this re-synthesized product and decomposing and undecomposed organic matter.
[0018]
The type of humus soil is not particularly limited, but the fallen leaves of deciduous trees and degradation products derived from animals are sufficiently degraded under a warm climate and then re-synthesized, and then saturated with calcium. It is desirable to use a humus soil made from the neutral humus produced as a raw material, reduced in molecular weight by biotechnology, and stabilized as a micelle colloid by increasing the amount. Neutral humus is a humus that has been buried underground in the ground for 8000 years, has a large amount of vegetative humus that is decomposed by microorganisms, and contains several tens of percent of fulvic acid and iron complex produced by biotechnology. Therefore, it is preferable.
[0019]
DETAILED DESCRIPTION OF THE INVENTION
DESCRIPTION OF EMBODIMENTS Hereinafter, an embodiment of a garbage disposal facility according to the present invention will be described with reference to the drawings, and a garbage disposal method by the treatment facility will also be described.
[0020]
FIG. 1 is a flowchart of the entire facility showing an embodiment of the garbage processing facility of the present invention.
As shown in FIG. 1, a garbage disposal facility 1 for biologically treating garbage B through activated sludge H containing humus soil J includes a garbage receiving hopper 2, a garbage wastewater storage tank (storage tank) 3 and the like. A biological treatment tank 4, a sludge culture tank 5, a humus soil supply machine 6, and a disinfection tank 7.
[0021]
The garbage receiving hopper 2 is closed at its upper end by an upper wall surface 2a, and has a loading port 2b for garbage B in a part of the upper wall surface 2a, and a lid 21 is attached to the loading port 2b so that it can be opened and closed. . An odor suction port 26 is formed in the center of the upper wall surface 2a, and one end of an odor suction tube 27 is connected to the suction port 26. Moreover, the lower end 2c of the hopper 2 is opened, and the rear side of the screw conveyor 23 communicates with the inside of the conveyor 23 in the lower end opening 2c. The screw conveyor 23 extends to above the garbage wastewater storage tank 3, and a garbage crusher 31 is connected to the front end of the screw conveyor 23. A drive motor 25 for the screw 24 is mounted at the rear end of the screw conveyor 23. The crusher 31 is provided with a drive motor 32 at the upper end, and an introduction cylinder 33 extends downward from the lower end opening. Further, in order to treat the garbage B in the same manner as the drainage, one end of the water supply pipe 11 for supplying fresh water (including water from the water supply) into the garbage receiving hopper 2 penetrates the upper wall surface 2a. Has been inserted. The other end of the water supply pipe 11 is connected to a water supply source (not shown).
[0022]
The storage tank 3 is a sealed tank whose upper end opening is closed by an upper wall surface 3a, and an introduction cylinder 33 of the pulverizer 31 passes through the upper wall surface 3a and faces the inside. An odor suction port 34 is formed in the center of the upper wall surface 3a, and one end of an odor suction tube 35 is connected to the suction port 34. A discharge pipe 36 for garbage sewage C is connected to the vicinity of the lower end of the side wall 3b of the storage tank 3, and a supply pump 40 is interposed in the discharge pipe 36 to measure the supply flow rate of the garbage sewage C ( The downstream end of the discharge pipe 36 is connected to the inlet of the flow meter 8. Further, one end of a drain pipe 37 for returning the garbage waste water C that has overflowed a preset flow rate (per unit time) to the storage tank 3 is connected to the measuring instrument 8, and the other end of the drain pipe 37 is connected to the storage tank 3. Is connected to the upper end of the side wall 3b. Further, a supply pipe 38 of the garbage sewage C is exposed to the inside of the biological treatment tank 4 from the outlet of the measuring instrument 8. The other end of the odor suction pipe 35 is connected to the middle of the odor suction pipe 27, and the other end of the odor suction pipe 27 is connected to the suction port of the blower 30.
[0023]
The biological treatment tank 4 has an open upper end, and in this example, the sludge H containing the humus soil J is in a range of 5000 to 15000 mg / l of sludge concentration with respect to the amount of stored garbage wastewater C. Is pre-loaded. Also, a submersible pump 41 is provided near the bottom of the biological treatment tank 4, and a sludge supply pipe is provided at the discharge port of the submersible pump 41 so that the sludge H deposited on the bottom can be supplied into the garbage receiving hopper 2. One end of 42 is connected, and the other end of the sludge supply pipe 42 is connected to the upper wall surface 2a of the garbage receiving hopper 2. One end of the sludge H discharge pipe 43 is connected to the upper end of the side wall 4 a of the biological treatment tank 4, and the other end is connected to the upper end of the side wall 5 b of the sludge culture tank 5. Furthermore, a submerged membrane device 9 is provided in the biological treatment tank 4 for separating the sludge H as a solid content from the garbage wastewater C and taking out the purified treated water x. The other end of the air introduction pipe 91 whose one end is connected to the discharge port of the blower 30 is connected to the bottom of the submerged membrane device 9, and the submerged membrane device 9 is discharged from the air introduction tube 91 (odor). In addition, the solid-liquid separation is promoted and air bubbles are discharged into the garbage wastewater C, and the microorganisms in the sludge H are ventilated to come into contact with the air. In addition, since the biological treatment tank 4 has opened the upper end, the upper surface of the garbage wastewater C is in contact with air.
[0024]
One end of the suction water supply pipe 71 for the treated water x is in contact with the upper end of the submerged membrane device 9, and a supply pump 72 is interposed in the middle of the suction water supply pipe 71. The other end of the suction water supply pipe 71 is the disinfection tank 7. In treated water x. In the disinfection tank 7, a storage container 73 for a solid disinfectant (sodium hypochlorite in this example) s is installed immediately below the outlet of the suction supply pipe 71, and a number of small containers provided in the storage container 73 are installed. The solid disinfectant s is dissolved in the treated water x from the holes. The dissolution concentration of the disinfectant s is set to about 10 PPM in this example. Thus, the sterilized treated water y is discharged into a sewer or a river in this example, but can be reused as a middle water.
[0025]
On the other hand, in addition to supplying the sludge H in the biological treatment tank 4 to the garbage receiving hopper 2 through the sludge supply pipe 42, the sludge H is also supplied from the discharge pipe 43 to the sludge culture tank 5. The upper end opening of the sludge culture tank 5 is blocked by the upper wall surface 5a, and the humus soil J is periodically supplied from the humus soil supply machine 6 to the sludge H in the sludge culture tank 5. The humus soil supply machine 6 includes a hopper-like container 61 in which the humus soil J is stored from the top inlet 62, a screw conveyor 64 disposed in communication with the lower end opening 63 of the container 61, and a front end of the screw conveyor 64. An introduction cylinder 67 is provided extending downward and penetrating through the upper wall surface 5a and facing the sludge H in the sludge culture tank 5. Moreover, the humus supply machine 6 is equipped with the screw 65 rotated with the motor 66 with which the rear end was equipped. In addition, the sludge density | concentration in the sludge culture tank 5 is set to 5000-15000 mg / l in this example. Further, the amount of sludge H fed from the biological treatment tank 4 to the sludge culture tank 5 is 50 to 100% by weight of the weight of the raw garbage B input to the raw garbage receiving hopper 2 for one day (24 hours). . Furthermore, the supply of the humus soil J supplied from the humus soil supply machine 6 for the activation of the sludge H in the sludge culture tank 5 is carried out at a rate of once every 20 to 30 days. Is 0.5 to 2.0% by weight of the input amount of garbage B. For this reason, the humus supply machine 6 is equipped with a timer (not shown), and the screw 65 is rotated by the motor 66 periodically for a certain period of time.
[0026]
A sludge supply pipe 51 is connected to the upper end portion of the side wall 3 b of the storage tank 3 in order to supply the activated sludge H to the storage tank 3 from an intermediate position in the vertical direction of the side wall 5 b of the sludge culture tank 5. One end of the branch pipe 44 branched in the middle of the sludge discharge pipe 43 is also connected to the upper end portion of the side wall of the storage tank 3, and the excess sludge H in the biological treatment tank 4 also passes through the branch pipe 44 to the storage tank 3. Supplied.
[0027]
In addition, the air introduction pipe 91 extending from the discharge port of the blower 30 is branched in the middle, and the branch pipe 92 is inserted to the vicinity of the bottom of the treated water x in the sterilization tank 7 and is connected to the lower end of the branch pipe 92. From the above, bubbled air is introduced into the treated water x. The air introduction pipe 91 is branched immediately downstream of the branch pipe 92, and the branch pipe 94 is inserted through the upper wall surface 3 a of the storage tank 3 to the vicinity of the bottom of the garbage wastewater C. Bubble air is introduced into the garbage waste water C from the air blowing nozzle 95 connected to the. Further, the branch pipe 94 is branched in the middle, and the second branch pipe 96 penetrates the upper wall surface 5a of the sludge culture tank 5, is inserted to the vicinity of the bottom in the sludge H, and is connected to the lower end of the second branch pipe 96. Air bubbles are introduced into the sludge H from the air blowing nozzle 97.
[0028]
Next, the operation state (garbage disposal method) of the embodiment of the garbage disposal facility having the above configuration will be described.
[0029]
1) For example, a large amount of garbage B generated from apartment houses such as condominiums and apartments, food factories, hotels, restaurants, etc., is transported directly or by garbage collection trucks and put into the garbage receiving hopper 2 .
[0030]
2) Fresh water is supplied from the water supply pipe 11 to the garbage receiving hopper 2 by 2 to 3 times (by weight) the amount of garbage B input. Also, the sludge H in the biological treatment tank 4 is supplied to the garbage receiving hopper 2 through the submersible pump 41 through the sludge supply pipe 42. The amount of sludge H supplied is around 30% of the weight of garbage B and water. When sludge H is mixed with garbage C, soil bacteria in the sludge produce metabolites. The product is a secretion of aerobic bacteria, facultative anaerobic bacteria, or a group of bacteria consisting of aerobic bacteria and facultative anaerobic bacteria, has an odor removal component, and the odor gas generated from garbage C is sludge H. , Reacts with odor components in the gas and decomposes to prevent the odor components from spreading and deodorize. Further, when air is introduced and aerated, aerobic bacteria contained in the sludge H, facultative anaerobic bacteria, or bacteria composed of aerobic bacteria and facultative anaerobic bacteria, A part is decomposed.
[0031]
3) The garbage B in the garbage receiving hopper 2 is mixed with water and sludge H and conveyed to the crusher 31 at the tip while being mixed and stirred by the screw conveyor 23 at the lower end. Then, the garbage B is finely pulverized by the pulverizer 31 and is mixed with the sludge H to be liquefied with fresh water, and is stored in the storage tank 3 as the garbage sewage C. In the storage tank 3, 30% by weight of sludge H is supplied from the biological treatment tank 4 and the sludge culture tank 6 with respect to the raw garbage sludge C, and is contained in the sludge H when air is introduced and aerated. The aerobic bacteria, facultative anaerobic bacteria, or a group of bacteria composed of aerobic bacteria and facultative anaerobic bacteria prevents the decomposition of garbage sewage C and the generation of malodors. In particular, since the sludge H supplied from the sludge culture tank 6 is activated by the input of the humus soil J, the deodorizing (deodorizing) effect and the decomposition action are excellent.
[0032]
4) The crushed material of the garbage B is decomposed to some extent and becomes close to sewage (drainage), and this trash sewage C is supplied to the biological treatment tank 4 by the supply pump while being metered at a predetermined flow rate by the measuring instrument. In the biological treatment tank 4, when the air is introduced and ventilated, the pulverized material of the garbage B is decomposed by microorganisms (soil fungi and the like) in the sludge H. And it decomposes | disassembles almost completely in the biological treatment tank 4, and turns into a carbon dioxide and water (treated water). The treated water x and the sludge H in the biological treatment tank 4 are separated from the sludge H by the submerged membrane device 9 that is vibrated by the air fed from the blower 30 and sucked by the supply pump 72 to be disinfected. 7 is sent. In addition, if the treated water x separated by the submerged membrane device 9 is equal to or less than a discharge standard value to the sewer (for example, BOD: 200 mg / l, SS: 200 mg / l and n-hexane: 10 mg / l or less), The treated water x can be discharged directly to the sewer or river without sending water to the disinfection tank 7.
[0033]
5) In the disinfecting tank 7, the treated water x is further disinfected by bubbling air from the air blowing nozzle 93 in a solution in which sodium hypochlorite s is dissolved at a concentration of about 10 PPM. The treated water y is drained from the drain pipe 75 and discharged.
[0034]
In addition, the sludge H sent from the biological treatment tank 4 to the sludge culture tank 5 is mixed with the humus soil J supplied from the humus soil supply machine 6, and the sludge H is contained in the humus soil J in the sludge culture tank 5. It is matured and humus activated by the action of the soil fungi. Further, in this example, the humus soil J used to activate the sludge H supplied from the humus soil feeder 6 contains humic acid with an organic content of 20% by weight or more, PH3 or less in an aqueous solution, and redox. Although the potential was +500 mmV or more, it goes without saying that the present invention is not limited to this.
[0035]
Another embodiment Although one embodiment related to the garbage processing facility of the present invention has been described above, it can be carried out as follows. That is,
(1) A grinder (disposer) is installed in the kitchen of each apartment in a condominium, such as a condominium, and the wastewater B is stored using the drain pipe while adding the water from the water supply while crushing the garbage B with the crusher. Directly sent to the tank 3 as raw garbage sewage C obtained by pulverizing the raw garbage B and adding water to liquefy it. Then, the sludge H, particularly activated sludge H, is supplied to the garbage wastewater storage tank 3 and mixed with the garbage wastewater C to decompose and deodorize the garbage B with microorganisms. In this case, the garbage receiving hopper 2 and the crew conveyor 23 with the garbage crusher 31 are not required.
[0036]
(2) In the biological treatment tank 4, the generation of surplus sludge is suppressed as much as possible. However, since surplus sludge is usually generated, this sludge H is dehydrated and stored except for the circulation, or the sludge culture tank 5 After humus soil J is activated by mixing and stirring, it can be dehydrated and dried to be used as a soil conditioner.
[0037]
【The invention's effect】
As is apparent from the above description, the garbage processing method and processing equipment according to the present invention have the following effects.
[0038]
(1) The invention according to claim 1 can treat raw garbage as water treatment in the same way as miscellaneous wastewater, so the treatment facility is relatively simple, and biodegradation of raw garbage by microorganisms in sludge is possible. Secondary pollution is prevented, and there is no odor or the like around the processing equipment, and the environment is not deteriorated. Furthermore, water mixed with raw garbage can be used as a sewer after treatment, and sludge generated in the treatment process can also be used as a soil conditioner, so there is no need for land for disposal or burial. Implementation is possible.
[0039]
In addition, since sludge is mainly used as a deodorization and biodegradation medium, maintenance costs are low, and since the sludge is circulated while being activated in the sludge culture tank, the deodorization and biodegradation effects do not decrease semipermanently. Can be used.
[0040]
(2) The invention described in claim 2 can surely implement the processing method of claim 1 and has substantially the same effect as the above-mentioned effect relating to claim 1, and has a relatively small number of constituent members and a simple structure. Equipment costs are also relatively low.
[0041]
(3) In the invention described in claim 3, by setting the sludge concentration to 5000 to 15000 mg / l, the sludge concentration necessary and sufficient for biological treatment of raw garbage is secured and the generation of excess sludge is minimized. Can be suppressed.
[Brief description of the drawings]
FIG. 1 is a flow chart of an entire facility showing an embodiment of a garbage disposal facility according to the present invention.
[Explanation of symbols]
DESCRIPTION OF SYMBOLS 1 Garbage processing equipment 2 Garbage receiving hopper 3 Garbage sewage storage tank 4 Biological treatment tank 5 Sludge culture tank 6 Humus soil supply machine 7 Disinfection tank 8 Meter (flow meter)
9 Submerged membrane device 23/64 Screw conveyor 27/35 Odor supply pipe 30 Blower 31 Garbage crusher 36/43 Drain pipe 37 Drain pipe 40/72 Supply pump 42 Sludge supply pipe 43 Sludge supply pipe 44/92/94 / 96 Branch pipe 51 Sludge supply pipe 61 Hopper container 71 Suction supply pipe 91 Air introduction pipe 93/95/97 Air outlet nozzle H Sludge J Humus soil B Garbage C Garbage wastewater x Treated water y Treated water s Disinfectant (next Sodium chlorite)

Claims (4)

生ゴミに腐植土を含む汚泥を混合して貯留し、この貯留した生ゴミの数倍の重量の水を生ゴミに加えて粉砕し、液状化した生ゴミ汚水を空気を導入しながら一定期間貯留したのち、腐植土を含む前記汚泥を混合撹拌して所定濃度に保った生物処理槽へ前記生ゴミ汚水を所定流量ずつ供給し、該生物処理槽内で前記生ゴミ汚水を、空気を導入して通気しながら前記汚泥中の微生物により分解処理したのち、固液分離して得られる処理水を下水道もしくは河川などに放流することを特徴とする生ゴミ処理方法。   Mixing and storing sludge containing humus soil in raw garbage, adding water several times the weight of the stored raw garbage to the raw garbage, crushing it, and introducing liquefied raw garbage wastewater for a certain period of time while introducing air After storage, the raw sludge containing the humus soil is mixed and stirred to supply a predetermined amount of the raw garbage wastewater to the biological treatment tank, and the raw wastewater is introduced into the biological treatment tank. Then, after decomposing with the microorganisms in the sludge while ventilating, the treated water obtained by solid-liquid separation is discharged into a sewer or a river, etc. 前記生物処理槽の汚泥濃度を、 5000〜15000mg/lに設定したことを特徴とする請求項1に記載の生ゴミ処理方法 The garbage disposal method according to claim 1, wherein the sludge concentration in the biological treatment tank is set to 5000 to 15000 mg / l . 生ゴミを投入するとともに腐植土を含む汚泥とともに生ゴミの数倍の重量の水を加えて貯留する生ゴミ受入れホッパーと、該ホッパー内の生ゴミを搬送するコンベヤ装置と、該コンベヤ装置の先端に連設され、粉砕して液状化する生ゴミ粉砕機と、粉砕、液状化された生ゴミ汚水を貯留する貯留タンクと、該貯留タンク内の生ゴミ汚水を所定量ずつ計量しながら生物処理槽へ供給する計量器と、腐植土を含む前記汚泥を前記生ゴミ汚水に混合撹拌して所定濃度に保った前記生物処理槽と、腐植土供給機を備え前記生物処理槽内の汚泥の一部を送給して貯留しながら活性化させる汚泥培養槽と、前記ホッパー内から臭気をあるいは大気中から空気を吸引し、前記貯留タンク、前記生物処理槽および前記汚泥培養槽に空気を送給する曝気用ブロワーと、前記生物処理槽内に配備される固液分離機構とを具備したことを特徴とする生ゴミ処理設備。 A garbage receiving hopper that throws in raw garbage and adds water several times the weight of raw garbage together with sludge containing humus soil, a conveyor device that conveys the raw garbage in the hopper, and a tip of the conveyor device A garbage pulverizer that is connected to the tank and pulverized and liquefied, a storage tank that stores pulverized and liquefied garbage sewage, and a biological treatment while measuring the amount of garbage sewage in the storage tank by a predetermined amount. A measuring instrument to be supplied to the tank; A sludge culture tank that is activated while being fed and stored, and sucks odors from the hopper or air from the atmosphere, and supplies air to the storage tank, the biological treatment tank, and the sludge culture tank Aeration blower If, garbage treatment facility, characterized by comprising a solid-liquid separation mechanism deployed in the biological treatment tank. 前記生物処理槽の汚泥濃度を、 5000〜15000mg/lに設定したことを特徴とする請求項3に記載の生ゴミ処理設備 The garbage disposal facility according to claim 3, wherein a sludge concentration in the biological treatment tank is set to 5000 to 15000 mg / l .
JP14269399A 1999-05-24 1999-05-24 Garbage disposal method and equipment Expired - Fee Related JP4328880B2 (en)

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CN104690075A (en) * 2015-03-13 2015-06-10 江西绿环生物科技有限公司 Carcass innocent treatment method

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KR100441917B1 (en) * 2001-04-28 2004-07-30 주식회사 드림바이오스 Automatic crushing and sorting equipment of garbage and method for sorting out foreign substance in the garbage
JP4928383B2 (en) * 2007-08-17 2012-05-09 株式会社富士環境整備 Garbage disposal equipment
JP2011062609A (en) * 2009-09-15 2011-03-31 Ibiden Co Ltd Method of treating garbage
JP2011062610A (en) * 2009-09-15 2011-03-31 Ibiden Co Ltd Method of treating garbage
CN104858217B (en) * 2015-05-30 2017-12-12 杭州扬中科技有限公司 A kind of life-garbage comprehensive treatment technology

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104690075A (en) * 2015-03-13 2015-06-10 江西绿环生物科技有限公司 Carcass innocent treatment method

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